System and method for conventional particle rounding utilizing continuous emulsion-aggregation (EA) technology
US-9372421-B2 · Jun 21, 2016 · US
US10989472B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10989472-B2 |
| Application number | US-201715498888-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 27, 2017 |
| Priority date | Apr 27, 2017 |
| Publication date | Apr 27, 2021 |
| Grant date | Apr 27, 2021 |
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Disclosed is a method, apparatus and system of drying wet toner particles which includes the use of cooling fluid. The method also includes introducing a heated drying gas into a toner drying chamber to create a circulating flow of drying gas.
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What is claimed is: 1. A toner drying apparatus comprising: a toner drying chamber including one or more curved inner radius portions; one or more drying gas inlets operatively connected to the toner drying chamber adapted to provide drying gas at a first temperature into the toner drying chamber and generate a circulating flow of chamber gas within the toner drying chamber; a toner feed inlet operatively connected to the toner drying chamber, the toner feed inlet adapted to feed wet toner particles into the circulating flow of chamber gas; one or more cooling fluid inlets operatively connected to the toner drying chamber adapted to provide cooling fluid at a second temperature less than the drying gas first temperature circulating flow of the chamber gas within the toner drying chamber; a toner outlet operatively connected to the toner drying chamber, the toner outlet adapted to direct an exiting stream of the chamber gas from the drying chamber generating exiting forces on dry toner particles in the circulating flow of chamber gas thereby transporting the dry toner particles from the toner drying chamber; and a controller operatively associated with the one or more drying gas inlets and the one or more cooling fluid inlets, the controller configured to control one or both of a flow rate and the second temperature of the cooling fluid provided into the toner drying chamber, thereby effecting a change in a temperature of the circulating flow of the chamber gas within the toner drying chamber, wherein the controller is configured to switch from a drying mode to a false load mode by injecting cooling fluid operating as a false load into the circulating flow of chamber gas as a feed rate of the wet toner particles ramps down. 2. The toner drying apparatus according to claim 1 , wherein the toner drying chamber is toroidal shaped. 3. The toner drying apparatus according to claim 1 , wherein the wet toner particles are associated with a chemical toner process. 4. The toner drying apparatus according to claim 1 , wherein the cooling fluid is water injected as a mist into the toner drying chamber. 5. The toner drying apparatus according to claim 1 , wherein the drying gas is air. 6. The toner drying apparatus according to claim 1 , wherein the controller is further configured to control one or more of the drying gas first temperature and a flow rate of the drying gas. 7. The toner drying apparatus according to claim 1 , wherein the controller is further configured to control one or both of the flow rate and the second temperature associated with the cooling fluid based on a feed rate of wet toner particles into the circulating flow of chamber gas. 8. The toner drying apparatus according to claim 1 , wherein the drying gas is provided into the toner drying chamber at a pressure of 1.0-psi (pounds per square inch) to 5.0-psi. 9. The toner drying apparatus according to claim 1 , wherein the drying gas is provided into the toner drying chamber at a rate of 3,000 feet per minute to 5,000 feet per minute. 10. The toner drying apparatus according to claim 1 , wherein the cooling fluid is provided into the toner dryer chamber at a pressure of 10-psi to 50-psi. 11. The toner drying apparatus according to claim 1 , wherein the cooling fluid is provided into the toner drying chamber at a rate of 1-litre/minute to 100-litres/minute. 12. The toner drying apparatus according to claim 1 , the controller configured to increase the temperature of the circulating flow of chamber gas as a total moisture content of the wet toner particles fed into the circulating flow of chamber gas increases, and decrease the temperature of the circulating flow of chamber gas as a total moisture content of the wet toner particles fed into the circulating flow of chamber gas decreases by injecting cooling fluid into the circulating flow of chamber gas. 13. The toner drying apparatus according to claim 1 , further comprising: a heat exchanger operatively connected to the drying gas and adapted to control the first temperature of the drying gas. 14. A toner dryer comprising: a toroidal shaped toner drying chamber including a plurality of curved inner radius portions; a plurality of drying air inlets operatively connected to the toner drying chamber adapted to provide drying air at a first temperature into the toner drying chamber and generate a circulating flow of chamber air within the toner drying chamber; a toner feed inlet operatively connected to the toner drying chamber, the toner feed inlet adapted to feed wet toner cakes into the toner drying chamber; a plurality of cooling fluid inlets operatively connected to the toner drying chamber adapted to inject water mist at a second temperature less than the first temperature into the toner drying chamber and into the circulating flow of the chamber air; a toner outlet operatively connected to the toner drying chamber, the toner outlet adapted to direct an exiting stream of the chamber air from the drying chamber generating exiting forces on dryer toner particles in the circulating flow of chamber air thereby transporting the dry toner particles from the toner drying chamber; and a controller operatively associated with the plurality of drying air inlets and the plurality of cooling fluid inlets, the controller configured to control a flow rate and the second temperature of the injected water mist into the toner drying chamber, thereby effecting a change in a temperature of the circulating flow of the chamber air within the toner drying chamber, wherein the controller is configured to increase the temperature of the circulating flow of chamber gas as a total moisture content of the wet toner particles fed into the circulating flow of chamber gas increases, and decrease the temperature of the circulating flow of chamber gas as a total moisture content of the wet toner particles fed into the circulating flow of chamber gas decreases by injecting cooling fluid into the circulating flow of chamber gas, wherein the controller is configured to preheat the toner drying chamber prior to feeding wet toner particles into the circulating flow of chamber gas, the controller configured to inject cooling fluid operating as a false load into the circulating flow of chamber gas and inject drying gas into the circulating flow of chamber gas, and wherein the controller is configured to switch from a drying mode to a false load mode by injecting cooling fluid operating as a false load into the circulating flow of chamber gas as a feed rate of the wet toner particles ramps down. 15. The toner drying apparatus according to claim 14 , wherein the wet toner particles are associated with a chemical toner process. 16. The toner drying apparatus according to claim 14 , wherein the drying gas is provided into the toner drying chamber at a pressure of 1.0-psi (pounds per square inch) to 5.0-psi. 17. The toner drying apparatus according to claim 14 , wherein the drying gas is provided into the toner drying chamber at a rate of 3,000 feet per minute to 5,000 feet per minute. 18. The toner drying apparatus according to claim 14 , wherein the cooling fluid is provided into the toner dryer chamber at a pressure of 10-psi to 50-psi. 19. The toner drying apparatus according to claim 14 , wherein the cooling fluid is provided into the toner drying chamber at a rate of 1-litre/minute to 100-litres/minute. 20. The toner drying apparatus according to claim 14 , further comprising: a heat exchanger operatively connected to the drying gas an
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